US10938050B2 - Membrane electrode assembly for fuel cells and manufacturing method thereof - Google Patents

Membrane electrode assembly for fuel cells and manufacturing method thereof Download PDF

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US10938050B2
US10938050B2 US15/818,662 US201715818662A US10938050B2 US 10938050 B2 US10938050 B2 US 10938050B2 US 201715818662 A US201715818662 A US 201715818662A US 10938050 B2 US10938050 B2 US 10938050B2
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electrolyte membrane
electrode assembly
membrane
peripheral region
water discharge
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US20180166721A1 (en
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Jong Kil Oh
Bo Ki Hong
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Hyundai Motor Co
Kia Corp
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Hyundai Motor Co
Kia Motors Corp
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    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1004—Fuel cells with solid electrolytes characterised by membrane-electrode assemblies [MEA]
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/02—Details
    • H01M8/0271—Sealing or supporting means around electrodes, matrices or membranes
    • H01M8/0273—Sealing or supporting means around electrodes, matrices or membranes with sealing or supporting means in the form of a frame
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/04—Auxiliary arrangements, e.g. for control of pressure or for circulation of fluids
    • H01M8/04082—Arrangements for control of reactant parameters, e.g. pressure or concentration
    • H01M8/04089—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants
    • H01M8/04119—Arrangements for control of reactant parameters, e.g. pressure or concentration of gaseous reactants with simultaneous supply or evacuation of electrolyte; Humidifying or dehumidifying
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/1041—Polymer electrolyte composites, mixtures or blends
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/1065—Polymeric electrolyte materials characterised by the form, e.g. perforated or wave-shaped
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M8/1016—Fuel cells with solid electrolytes characterised by the electrolyte material
    • H01M8/1018—Polymeric electrolyte materials
    • H01M8/1069—Polymeric electrolyte materials characterised by the manufacturing processes
    • H01M8/1086—After-treatment of the membrane other than by polymerisation
    • H01M8/1088—Chemical modification, e.g. sulfonation
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/24—Grouping of fuel cells, e.g. stacking of fuel cells
    • H01M8/241—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes
    • H01M8/242—Grouping of fuel cells, e.g. stacking of fuel cells with solid or matrix-supported electrolytes comprising framed electrodes or intermediary frame-like gaskets
    • H—ELECTRICITY
    • H01—ELECTRIC ELEMENTS
    • H01M—PROCESSES OR MEANS, e.g. BATTERIES, FOR THE DIRECT CONVERSION OF CHEMICAL ENERGY INTO ELECTRICAL ENERGY
    • H01M8/00—Fuel cells; Manufacture thereof
    • H01M8/10—Fuel cells with solid electrolytes
    • H01M2008/1095—Fuel cells with polymeric electrolytes
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30—Hydrogen technology
    • Y02E60/50—Fuel cells
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P70/00—Climate change mitigation technologies in the production process for final industrial or consumer products
    • Y02P70/50—Manufacturing or production processes characterised by the final manufactured product

Definitions

  • the present disclosure relates to a membrane electrode assembly for fuel cells and a manufacturing method thereof. More particularly, the present disclosure relates to a membrane electrode assembly for fuel cells capable of preventing water in an electrolyte membrane of the membrane electrode assembly from diffusing to a peripheral region of the electrolyte membrane, which is outside an active area of a fuel cell, thereby preventing loss of the water used for fuel cell reaction in the electrolyte membrane, to improve efficiency in handling of water in the fuel cell, and to improve corrosion resistance of a stack and a manufacturing method thereof.
  • a fuel cell is a power generation device that induces an electrochemical reaction between fuel gas and oxidizing gas to convert chemical energy in fuel into electrical energy.
  • Such a fuel cell is widely used for a power source in industries, homes, and vehicles.
  • the fuel cell may also be used to supply power to small-sized electric/electronic products or portable devices.
  • the polymer electrolyte membrane fuel cell is used as a power source for supplying power to a motor for driving a fuel cell vehicle and various kinds of electric devices of the fuel cell vehicle.
  • hydrogen is used as fuel gas
  • oxygen or air including oxygen is used as oxidizing gas.
  • the fuel cell includes a cell in which the fuel gas and the oxidizing gas react with each other to generate electrical energy.
  • a plurality of cells is stacked and connected to each other in series in the form of a stack to satisfy power requirements.
  • the fuel cell for vehicles requires high power. For this reason, several hundred unit cells, each of which generates electrical energy, are stacked in the form of a stack.
  • Each unit cell of the polymer electrolyte membrane fuel cell includes a membrane electrode assembly (MEA), which includes a polymer electrolyte membrane capable of moving protons and electrodes attached to opposite surfaces of the polymer electrolyte membrane, a gas diffusion layer (GDL) for supplying reaction gases, such as fuel gas and oxidizing gas, to the membrane electrode assembly and transmitting generated electrical energy, a gasket for maintaining airtightness of the reaction gases and coolant, a fastening member for maintaining appropriate fastening pressure, and a bipolar plate (BP) for moving the reaction gases and the coolant.
  • MEA membrane electrode assembly
  • GDL gas diffusion layer
  • BP bipolar plate
  • the membrane electrode assembly includes a polymer electrolyte membrane capable of moving protons and an anode and a cathode attached to opposite surfaces of the polymer electrolyte membrane, a catalyst for inducing a reaction between hydrogen, which is fuel gas, and air (or oxygen), which is oxidizing gas, being applied to the anode and the cathode.
  • a gas diffusion layer (GDL) for uniformly distributing the fuel gas and the oxidizing gas is stacked on the outside of the membrane electrode assembly, i.e. the outside of each of the anode and the cathode, and a bipolar plate for providing a channel, along which reaction gases and coolant flow, and supplying the reaction gases to the gas diffusion layer is disposed at the outside of the gas diffusion layer.
  • GDL gas diffusion layer
  • a gasket for fluid sealing is disposed between parts constituting unit cells.
  • the gasket may be integrally formed with the membrane electrode assembly or the bipolar plate.
  • the above elements constitute a unit cell.
  • a plurality of cells is stacked, end plates for supporting the cells are coupled to the outermost ends of the stacked cells, and the end plates are fastened to the cells using a stack fastening member to constitute a fuel cell stack.
  • a reaction in the fuel cell for generating electrical energy is performed in a membrane electrode assembly (MEA) including a perfluorinated sulfonic acid (PFSA) electrolyte membrane and electrodes, such as an anode and a cathode.
  • MEA membrane electrode assembly
  • PFSA perfluorinated sulfonic acid
  • fuel gas i.e. hydrogen
  • anode which is an oxidation electrode (i.e. a fuel electrode) of the fuel cell
  • protons move to the cathode, which is a reduction electrode (i.e. an air electrode) through the electrolyte membrane.
  • Oxygen molecules, protons, and electrons react together at the cathode, with the result that electricity and heat are generated.
  • water is generated as a reaction by-product.
  • the flooded water prevents reaction gases from being efficiently supplied into the unit cells of the fuel cell, whereby voltage loss is further increased.
  • compression pressure generated by the gasket, which is made of a rubber elastomer, is applied to the membrane electrode assembly for a long time.
  • the shape of the membrane electrode assembly must be maintained without being tom or deformed even when the membrane electrode assembly is compressed for a long time.
  • membrane electrode assemblies may be used for a long time even when several hundred membrane electrode assemblies are stacked in one stack.
  • an electrolyte membrane is manufactured such that, in addition to an active area, in which a cathode and an anode, which are used to induce an electrochemical reaction in the fuel cell, are bonded to the electrolyte membrane, an extended region is formed outside the active area of the fuel cell in order to securely bond the subgasket to the electrolyte membrane.
  • the subgasket is bonded to the extended region, i.e. a peripheral region, of the electrolyte membrane.
  • the diffused water may corrode the other parts of the stack that are made of metal materials, whereby the stability in travel of the vehicle may be greatly lowered.
  • reaction gases and the coolant may leak due to the step between the region of the subgasket to which the electrolyte membrane is bonded and the region of the subgasket to which the electrolyte membrane is not bonded.
  • the membrane and the subgasket may be separated from each other after operation of the fuel cell for a long time, with the result that the operation of the fuel cell may be stopped.
  • the present disclosure has been made in an effort to solve the above-described problems associated with the related art.
  • the present disclosure is directed to providing a membrane electrode assembly for fuel cells configured such that it is possible to prevent water in an electrolyte membrane of the membrane electrode assembly from diffusing to a peripheral region of the electrolyte membrane, which is outside an active area of a fuel cell, thereby preventing the loss of the water used for fuel cell reaction in the electrolyte membrane, to improve efficiency in handling of water in the fuel cell, and to improve corrosion resistance of a stack and a manufacturing method thereof.
  • a membrane electrode assembly for fuel cells includes: an electrolyte membrane; a cathode and an anode, each being stacked on the electrolyte membrane; and subgaskets bonded to a peripheral region of the electrolyte membrane, which is outside an active area, in which the cathode and the anode are stacked on the electrolyte membrane.
  • the electrolyte membrane is provided in at least a portion of the peripheral region of the electrolyte membrane, which is outside the active area, with a water discharge blocking region for preventing water in the electrolyte membrane from diffusing and being discharged to the outside.
  • a method of manufacturing a membrane electrode assembly for fuel cells includes: applying a metal cation solution, having a metal cation precursor dissolved in a solvent, to at least a selected portion of a peripheral region of an electrolyte membrane, which is outside an active area of the electrolyte membrane, in which a cathode and an anode are stacked on the electrolyte membrane, to form a water discharge blocking region; stacking the cathode and the anode on the active area of the electrolyte membrane; and stacking subgaskets on the peripheral region of the electrolyte membrane, which is outside the active area, in which the cathode and the anode are stacked on the electrolyte membrane.
  • the water discharge blocking region is formed as a result of protons coupled in a sulfonic acid group (—SO 3 ⁇ H + ) of the electrolyte membrane being substituted by metal cations in the solution.
  • vehicle or “vehicular” or other similar term as used herein is inclusive of motor vehicles in general such as passenger automobiles including sports utility vehicles (SUV), buses, trucks, various commercial vehicles, watercraft including a variety of boats and ships, aircraft, and the like, and includes hybrid vehicles, electric vehicles, plug-in hybrid electric vehicles, hydrogen-powered vehicles and other alternative fuel vehicles (e.g. fuels derived from resources other than petroleum).
  • a hybrid vehicle is a vehicle that has two or more sources of power, for example both gasoline-powered and electric-powered vehicles.
  • FIG. 1 shows a membrane electrode assembly according to an embodiment of the present disclosure
  • FIG. 2 shows a membrane electrode assembly according to another embodiment of the present disclosure.
  • FIG. 3 shows a membrane electrode assembly according to a further embodiment of the present disclosure.
  • the present disclosure provides a membrane electrode assembly for fuel cells configured such that it is possible to prevent water in an electrolyte membrane of the membrane electrode assembly from diffusing to a peripheral region of the electrolyte membrane, which is outside an active area of a fuel cell without reduction of fuel cell operation performance and damage to airtightness, thereby preventing the loss of the water used for fuel cell reaction in the electrolyte membrane, to improve efficiency in handling of water in the fuel cell, and to improve corrosion resistance of a stack and a manufacturing method thereof.
  • FIG. 1 is a plan view and sectional views showing a membrane electrode assembly according to an embodiment of the present disclosure.
  • a membrane electrode assembly (MEA) 10 which is used in a polymer electrolyte membrane fuel cell (PEMFC), includes a polymer electrolyte membrane 11 capable of moving protons, an anode 13 and a cathode 12 attached to opposite surfaces of the polymer electrolyte membrane 11 , a catalyst for inducing a reaction between hydrogen, which is fuel gas, and air (or oxygen), which is oxidizing gas, being applied to the anode 13 and the cathode 12 , and subgaskets 14 bonded to opposite surfaces of a peripheral region of the polymer electrolyte membrane 11 .
  • PEMFC polymer electrolyte membrane fuel cell
  • the membrane electrode assembly 10 has an area in which the anode 13 and the cathode 12 are bonded to the polymer electrolyte membrane 11 , which is an area in which an electrochemical reaction occurs, i.e. an active area, to which the fuel gas and the oxidizing gas are supplied such that a reaction occurs in a fuel cell.
  • the cathode 12 and the anode 13 are attached to opposite surfaces of the membrane electrode assembly 10 , and the area in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11 is an active area, in which reaction occurs in the fuel cell.
  • subgaskets 14 are bonded to the peripheral region of the polymer electrolyte membrane 11 excluding the active area, in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11 .
  • the subgaskets 14 may be bonded to the entire peripheral region of the polymer electrolyte membrane 11 excluding the active area.
  • FIG. 1 is a plan view of the membrane electrode assembly.
  • FIG. 1 is a sectional view taken along line X-X of the plan view and a sectional view taken along line Y-Y of the plan view.
  • line X-X may be a line extending in a longitudinal direction of the membrane electrode assembly 10 while passing through the active area
  • line Y-Y may a line extending in the lateral direction of the membrane electrode assembly 10 while passing through the active area.
  • the active area of the membrane electrode assembly 10 in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11 , is located in the middle of the membrane electrode assembly in a rectangular shape.
  • each subgasket 14 is bonded to the peripheral region of the polymer electrolyte membrane 11 excluding the middle active area, in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11 .
  • Each subgasket 14 has a rectangular opening formed in the middle thereof such that the middle active area is exposed through the opening, i.e. such that the cathode 12 and the anode 13 are exposed, through the opening.
  • each subgasket 14 is formed in a rectangular frame shape such that each subgasket 14 is located at the rectangular edge of the membrane electrode assembly 10 .
  • the subgaskets 14 may be stacked and bonded to the opposite surfaces of the polymer electrolyte membrane 11 at the peripheral region of the polymer electrolyte membrane 11 , which is outside the cathode 12 and the anode 13 (i.e. the active area) such that the subgaskets 14 do not overlap the cathode 12 or the anode 13 .
  • the membrane electrode assembly 10 further includes a water discharge blocking region 11 a formed in at least a portion of the peripheral region of the polymer electrolyte membrane 11 , to which the subgaskets 14 are bonded.
  • the water discharge blocking region 11 a is configured to prevent water in the polymer electrolyte membrane 11 from moving to the peripheral region of the polymer electrolyte membrane 11 , which is outside the active area, due to diffusion thereof. That is, the water discharge blocking region 11 a prevents water used for reaction in the fuel cell from diffusing to the peripheral region of the polymer electrolyte membrane 11 and being discharged out of the fuel cell, thereby preventing the water from being lost.
  • the water discharge blocking region 11 a By the provision of the water discharge blocking region 11 a , it is possible to prevent the movement and diffusion of water to the peripheral region of the polymer electrolyte membrane 11 and the discharge of the water to the outside, thereby preventing loss of the water. Consequently, it is possible to prevent a stack from being corroded by water discharged from each cell, thereby improving the corrosion resistance of the stack. In addition, it is possible to improve efficiency in handling of water in the fuel cell.
  • the water discharge blocking region 11 a is formed in the peripheral region of the polymer electrolyte membrane 11 , to which the subgaskets 14 are bonded, by additional processing. After the processing, the peripheral region of the polymer electrolyte membrane 11 may perform a water discharge blocking function.
  • the water discharge blocking region 11 a may extend along sides of the polymer electrolyte membrane 11 at the peripheral region of the polymer electrolyte membrane 11 so as to have a predetermined width. As illustrated in FIG. 1 , the water discharge blocking region 11 a may extend along the entire peripheral region of the polymer electrolyte membrane 11 so as to have a rectangular frame shape.
  • the water discharge blocking region 11 a is formed in a portion of the peripheral region of the polymer electrolyte membrane 11 that is spaced apart from the active area by a predetermined distance so as to have a predetermined width.
  • the subgaskets 14 are stacked and bonded to the water discharge blocking region 11 a of the polymer electrolyte membrane 11 .
  • the water discharge blocking region 11 a is formed in the polymer electrolyte membrane 11 along four sides of the membrane electrode assembly 10 , i.e. two long sides and two short sides thereof, so as to have a predetermined width at each side.
  • the water discharge blocking region 11 a is formed in a rectangular frame shape.
  • the width of the water discharge blocking region 11 a of the polymer electrolyte membrane 11 may be 0.5 times or less the total width of the peripheral region of the polymer electrolyte membrane 11 .
  • the water discharge blocking region 11 a of the polymer electrolyte membrane 11 is formed in a portion of the peripheral region of the polymer electrolyte membrane 11 excluding the active area (i.e. the electrochemical reaction area), in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11 , i.e. the region in which the subgaskets are bonded to the polymer electrolyte membrane 11 , spaced apart from the active area by a predetermined distance set at each side.
  • the width of the water discharge blocking region 11 a at an arbitrary position of each side may be 0.5 times or less the total width of the region in which the subgaskets are bonded to the polymer electrolyte membrane 11 at the same position.
  • the water discharge blocking region 11 a is greater than 0.5 times the total width of the region in which the subgaskets are bonded to the polymer electrolyte membrane 11 , the water discharge blocking region 11 a , which is formed by metal cation substitution, as will be described below, is too close to the active area (i.e. the electrochemical reaction area), with the result that electrochemical reaction (i.e. fuel cell reaction) may be affected.
  • the water discharge blocking region 11 a may be formed in a portion of the peripheral region of the polymer electrolyte membrane 11 , more specifically, only two opposite sides of the polymer electrolyte membrane 11 , among the four sides of the polymer electrolyte membrane 11 .
  • FIGS. 2 and 3 show embodiments in which the water discharge blocking region 11 a is formed in only two opposing sides of the polymer electrolyte membrane 11 .
  • FIG. 2 shows an embodiment in which the water discharge blocking region 11 a is formed in only two opposing long sides of the polymer electrolyte membrane 11 , among the four sides of the polymer electrolyte membrane 11 .
  • FIG. 3 shows an embodiment in which the water discharge blocking region 11 a is formed in only two opposing short sides of the polymer electrolyte membrane 11 , among the four sides of the polymer electrolyte membrane 11 .
  • the water discharge blocking region 11 a may be spaced apart from the active area by a predetermined distance at each side, as described above. Even in the embodiments of FIGS. 2 and 3 , the width of the water discharge blocking region 11 a at an arbitrary position of each side may be 0.5 times or less the total width of the region in which the subgaskets are bonded to the polymer electrolyte membrane 11 at the same position.
  • the width of the water discharge blocking region 11 a at an arbitrary position of each side may be less than the distance from the active area.
  • the water discharge blocking region 11 a is spaced apart from the active area, in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11 and that the peripheral region of the polymer electrolyte membrane 11 (i.e. the region in which the subgaskets 14 are bonded to the polymer electrolyte membrane 11 ) outside the active area of the polymer electrolyte membrane 11 is divided into a portion forming the water discharge blocking region 11 a and a portion forming only the polymer electrolyte membrane 11 .
  • the water discharge blocking region 11 a may be formed by applying a solution containing metal cations to the polymer electrolyte membrane 11 such that protons coupled in a sulfonic acid group (—SO 3 ⁇ H + ) of the polymer electrolyte membrane 11 are substituted by the metal cations.
  • the water discharge blocking region 11 a for blocking the movement of water may be formed in the polymer electrolyte membrane 11 .
  • the property of a portion of the peripheral region of the polymer electrolyte membrane 11 corresponding to the water discharge blocking region 11 a is changed by selective cation substitution such that a specific region in the polymer electrolyte membrane 11 forms the water discharge blocking region 11 a.
  • the water discharge blocking region 11 a is realized by changing the property of a portion of the region in which the subgaskets 14 are bonded to the polymer electrolyte membrane 11 by cation substitution. Consequently, the water discharge blocking region 11 a blocks the movement of water in the polymer electrolyte membrane 11 to the outside, whereby it is possible to prevent the water from being discharged to the outside.
  • protons coupled in a sulfonic acid group (—SO 3 ⁇ H + ) of the membrane are substituted by cations, which exhibit higher affinity for a sulfonic group (—SO 3 ⁇ ) of the membrane than the protons, to disturb coupling between the protons and water molecules.
  • the water content of the membrane may be reduced without affecting the fuel cell reaction, thereby greatly reducing the amount of water discharged out of the membrane electrode assembly.
  • the polymer electrolyte membrane 11 includes a water discharge blocking region 11 a formed in the peripheral region of the polymer electrolyte membrane 11 outside the active area by selective cation substitution.
  • the water discharge blocking region 11 a in the polymer electrolyte membrane 11 is formed in at least a portion of the outer part of the region in which the subgaskets 14 are bonded to the polymer electrolyte membrane 11 , excluding the active area, which is an electrochemical reaction part.
  • a method of forming the water discharge blocking region 11 a in a selected region of the polymer electrolyte membrane 11 opposite surfaces of the polymer electrolyte membrane 11 , excluding the water discharge blocking region 11 a , are covered with a masking member (not shown), and a metal cation solution having a metal cation precursor dissolved in a solvent is applied to the exposed region of the polymer electrolyte membrane 11 , which is not covered by the masking member, through a wet process, such as spraying, brushing, or rolling.
  • the water discharge blocking region may be simultaneously formed in the peripheral region of the polymer electrolyte membrane outside the active area of the cell by spraying a metal cation solution to the side surfaces of a fuel cell stack after assembling the fuel cell stack.
  • the present disclosure is not limited thereto.
  • the metal (M) cation solution may include a metal cation precursor represented by [Chemical Formula 1] below and a solvent.
  • M(X) n [Chemical Formula 1]
  • M may be selected from a group consisting of Na, Li, K, Ca, Mg, Cu, Zn, Ni, Fe, Cr, and Al
  • X may be selected from a group consisting of chloride, sulfate, acetate, nitrate, hydroxide, and a combination thereof.
  • n is set based on the valence of M.
  • the metal cation solution may include one or more metal cation precursors.
  • the metal cations, generated from the metal (M), may be bivalent metal cations. More specifically, the metal cations may be bivalent or trivalent metal cations.
  • the concentration of the metal cations in the solution may be at least 1 mol %. If the concentration of the metal cations is less than 1 mol %, cation substitution is not sufficiently performed, with the result that water discharge blocking efficiency may be reduced.
  • the solvent is used to dissolve the metal cation precursor.
  • One or a mixture of two or more selected from a group consisting of de-ionized water, methanol, ethanol, iso-propyl alcohol, 1-propanol, and 2-methoxyethanol may be used as the solvent.
  • De-ionized water may be used.
  • the polymer electrolyte membrane 11 is dried and the masking member is removed for a time sufficient to perform cation substitution.
  • the polymer electrolyte membrane 11 may be dried using a natural drying method. Alternatively, a hot air drying method or a vacuum drying method may be used in order to reduce drying time.
  • the masking member is removed to obtain the polymer electrolyte membrane 11 , the cathode 12 and the anode 13 are stacked on the polymer electrolyte membrane 11 , and the subgaskets 14 are stacked and bonded to the polymer electrolyte membrane 11 using an ordinary process.
  • the water discharge blocking region 11 a may be formed.
  • the water discharge blocking region which is formed by metal cation substitution, is formed in the peripheral region of the polymer electrolyte membrane, which is outside the active area of the membrane electrode assembly, whereby it is possible to achieve an excellent handling property owing to the subgaskets, which is required of the membrane electrode assembly, to maintain the airtightness of the fuel cell, and to prevent the diffusion of water to the peripheral region of the fuel cell through the use of the water discharge blocking region.
  • A′ and A′′ indicate the electrochemical reaction part, i.e. the active area of the membrane electrode assembly, in which the cathode 12 and the anode 13 are bonded to the polymer electrolyte membrane 11
  • B′ and B′′ indicate the region in which the subgaskets 14 are bonded to the polymer electrolyte membrane 11 , i.e. the peripheral region of the polymer electrolyte membrane 11 , which is outside the active area.
  • A′ indicates the length of the active area
  • A′′ indicates the width of the active area
  • B′ indicates the width of the peripheral region at each short side
  • B′′ indicates the width of the peripheral region at each long side.
  • B 1 ′ and B 1 ′′ indicate a portion of the peripheral region of the polymer electrolyte membrane 11 in which cation substitution has not been performed, i.e. a cation un-substitution region, which is provided to separate the active area of the polymer electrolyte membrane 11 and the water discharge blocking region 11 a from each other.
  • B 1 ′ indicates the width of the cation un-substitution region at each short side (i.e. the distance between the active area the water discharge blocking region), and B 1 ′′ indicates the width of the cation un-substitution region at each long side (i.e. the distance between the active area the water discharge blocking region).
  • B 2 ′ and B 2 ′′ indicate the water discharge blocking region 11 a of the polymer electrolyte membrane 11 , which is formed by selective cation substitution.
  • the water discharge blocking region 11 a is formed at four sides of the polymer electrolyte membrane 11 .
  • the water discharge blocking region 11 a is formed at two opposing long sides of the polymer electrolyte membrane 11 .
  • the water discharge blocking region 11 a is formed at two opposing short sides of the polymer electrolyte membrane 11 .
  • B 2 ′ ⁇ 0.5 ⁇ B′ and B 2 ′′ ⁇ 0.5 ⁇ B′′ are shown in the embodiment of FIG. 1
  • B 2 ′′ ⁇ 0.5 ⁇ B′′ is shown in the embodiment of FIG. 2 .
  • the water discharge blocking region which is formed by metal cation substitution, is formed in the peripheral region of the polymer electrolyte membrane, which is outside the active area of the membrane electrode assembly, whereby it is possible to achieve an excellent handling property due to the subgaskets, which is required of the membrane electrode assembly, to maintain the airtightness of the fuel cell, and to prevent the diffusion of water to the peripheral region of the fuel cell through the use of the water discharge blocking region.

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KR20180067988A (ko) 2018-06-21
KR102518684B1 (ko) 2023-04-05
DE102017220812A1 (de) 2018-06-14

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